JP2016216697A - Production method of water-added fuel oil, and water-added fuel oil - Google Patents

Production method of water-added fuel oil, and water-added fuel oil Download PDF

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JP2016216697A
JP2016216697A JP2015112650A JP2015112650A JP2016216697A JP 2016216697 A JP2016216697 A JP 2016216697A JP 2015112650 A JP2015112650 A JP 2015112650A JP 2015112650 A JP2015112650 A JP 2015112650A JP 2016216697 A JP2016216697 A JP 2016216697A
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JP6464456B2 (en
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博道 吉田
Hiromichi Yoshida
博道 吉田
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Keihin Plantech Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a production method of water-added fuel oil useful for spreading water-added fuel oil that shares two passages for circulating water and water-added fuel oil and thus reduces parts for a simple structure and can be easily applied to an existing facility, and to provide water-added fuel oil.SOLUTION: A production method of water-added fuel oil includes a first step for reducing raw water in an oxidation/reduction apparatus 8 and circulating the reduced water to a water tank 1 through a first circuit 12 equipped with a high pressure pump 6 and a line mixer 7 for a required time, a second step for circulating mixed oil of raw oil and an additive to a mixed oil tank 4 through a second circuit 13 equipped with the high pressure pump 6 and the line mixer 7 for another required time and then further circulating a mixture of the reduced water circulated in the first step and the mixed oil circulated through the second circuit, through the second circuit 13 for another required time, and a third step for leaving water-added fuel oil emulsified in the mixed oil tank 4 for standing in an oily water standing tank 5 for another required time and then sending the water-added fuel oil for burning in a furnace F.SELECTED DRAWING: Figure 1

Description

発明の詳細な説明Detailed Description of the Invention

この発明は、水と燃料油より加水燃料油を生成し、これを燃焼装置に供給可能な加水燃料油の製造方法および加水燃料油に関するものである。  TECHNICAL FIELD The present invention relates to a method for producing a hydrolyzed fuel oil capable of producing hydrous fuel oil from water and fuel oil and supplying it to a combustion device, and a hydrolyzed fuel oil.

近年、例えば重油の中に水を微粒子状に分散させた燃料油が、重油の燃焼費の節約や、燃焼排気ガス中のNOx、SOxの減少等の効果を有することから注目され検討されている。  In recent years, for example, fuel oil in which water is dispersed in the form of fine particles in heavy oil has attracted attention and has been studied because it has effects such as saving fuel costs of heavy oil and reducing NOx and SOx in combustion exhaust gas. .

そこで、特許文献1に示す加水燃料油の製造方法は、透過度や安定性を高め、長時間の貯蔵をしても安定した状態を維持でき、かつ、透明性のある商品価値の高い加水燃料油を得ることができる。  Therefore, the method for producing a hydrolyzed fuel oil shown in Patent Document 1 increases the permeability and stability, can maintain a stable state even after long-term storage, and has a high commercial value with transparency. Oil can be obtained.

しかしながら、上記のような加水燃料油の製造方法では、振動波によって励起させた天然鉱物とか、加熱・加圧手段などを備えたプラントシステムよりなり、構造が複雑で設備が大型化し、加水燃料油の価格が高騰するなどの問題がある。  However, the above-described method for producing a hydrolyzed fuel oil comprises a plant system equipped with natural minerals excited by vibration waves, heating / pressurizing means, etc., and has a complicated structure and large equipment. There are problems such as rising prices.

特許第4682287号公報Japanese Patent No. 4682287

この発明は、以上のようなことを考慮してなされたもので、水と加水燃料油を循環する二つの流路を互いに併用することにより、部品点数を削減して構造を簡素化し、既存の設備にも容易に適用可能として、燃焼安定性のある加水燃料油を生成する加水燃料油の製造方法および加水燃料油を提供することを目的とする。  The present invention has been made in consideration of the above, and by using two flow paths for circulating water and water-added fuel oil together, the number of parts is reduced and the structure is simplified. It is an object of the present invention to provide a method for producing a hydrolyzed fuel oil that can be easily applied to facilities, and to produce a hydrolyzed fuel oil having combustion stability and a hydrolyzed fuel oil.

前記課題を解決し、かつ目的を達成するために、この発明は、以下の様に構成した。  In order to solve the above problems and achieve the object, the present invention is configured as follows.

請求項1に記載の発明は、原水を酸化還元装置により還元した後、この還元水を、水タンクに高圧ポンプとラインミキサーとが接続される第1循環路にて所要時間循環させる第1工程と、原料油と添加剤との混合油を、混合油タンクに前記高圧ポンプと前記ラインミキサーとが接続される第2循環路にて所要時間循環させた後、前記第1工程にて循環させた前記還元水と、前記第2循環路で循環させた前記混合油との混合油水を前記第2循環路にてさらに所要時間循環させる第2工程と、前記混合油タンク内にてエマルジョン化した加水燃料油を油水静置タンク内で所要時間静置させ、燃焼装置の燃料油として送り出す第3工程とを含むことを特徴とする加水燃料油の製造方法である。  In the first aspect of the present invention, after the raw water is reduced by the redox device, the reduced water is circulated for a required time in a first circulation path in which a high pressure pump and a line mixer are connected to the water tank. And the mixed oil of the raw material oil and the additive is circulated in the first step after being circulated for a required time in the second circulation path where the high pressure pump and the line mixer are connected to the mixed oil tank. A second step of circulating a mixed oil water of the reduced water and the mixed oil circulated in the second circulation path for a further required time in the second circulation path; and emulsification in the mixed oil tank. And a third step of allowing the hydrolyzed fuel oil to stand for a required time in an oil-water static tank and sending it out as a fuel oil for the combustion apparatus.

請求項2に記載の発明は、上記請求項1に記載の加水燃料油の製造方法において、原料油は、石油系液体燃料からなることを特徴とする加水燃料油の製造方法である。  The invention according to claim 2 is the method for producing hydrolyzed fuel oil according to claim 1, wherein the feedstock oil is composed of petroleum liquid fuel.

請求項3に記載の発明は、上記請求項1乃至2の何れか1項に記載の加水燃料油の製造方法において、混合油には酵素を混入することを特徴とする加水燃料油の製造方法である。  Invention of Claim 3 is the manufacturing method of the hydrofuel oil of any one of the said Claim 1 thru | or 2, The enzyme is mixed in mixed oil, The manufacturing method of the hydrofuel oil characterized by the above-mentioned. It is.

請求項4に記載の発明は、請求項1乃至3の何れか1項に記載の加水燃料油の製造方法により生成してあり、加水燃料油内の原料油の量を65〜75%の割合にしてなることを特徴とする加水燃料油である。  Invention of Claim 4 is produced | generated by the manufacturing method of the hydrolyzed fuel oil of any one of Claims 1 thru | or 3, The amount of the raw material oil in hydrous fuel oil is a ratio of 65 to 75% It is the water fuel oil characterized by the above-mentioned.

前記構成により、この発明は、以下のような効果を有する。  With the above configuration, the present invention has the following effects.

請求項1に記載の発明では、原水を酸化還元装置により還元した後、この還元水を、水タンクに高圧ポンプとラインミキサーとが接続される第1循環路にて所要時間循環させる第1工程と、原料油と添加剤との混合油を、混合油タンクに前記高圧ポンプと前記ラインミキサーとが接続される第2循環路にて所要時間循環させた後、前記第1工程にて循環させた前記還元水と、前記第2循環路で循環させた前記混合油との混合油水を前記第2循環路にてさらに所要時間循環させる第2工程と、前記混合油タンク内にてエマルジョン化した加水燃料油を油水静置タンク内で所要時間静置させ、燃焼装置の燃料油として送り出す第3工程とよりなるので、還元水や混合油の通過する流路を併用して簡便としながら、前記燃焼装置の始動時には油分の高い燃料を燃焼部へと送出することができ、既存の設備にも容易に適用可能となる。  In the first aspect of the present invention, after the raw water is reduced by the redox device, the reduced water is circulated for a required time in a first circulation path in which a high pressure pump and a line mixer are connected to the water tank. And the mixed oil of the raw material oil and the additive is circulated in the first step after being circulated for a required time in the second circulation path where the high pressure pump and the line mixer are connected to the mixed oil tank. A second step of circulating a mixed oil water of the reduced water and the mixed oil circulated in the second circulation path for a further required time in the second circulation path; and emulsification in the mixed oil tank. Since the hydrolyzed fuel oil is allowed to stand in the oil-water static tank for a required time and is sent out as a fuel oil for the combustion apparatus, it is a third step. When starting the combustion equipment, There fuel can be delivered to the combustion section, and readily applicable to existing installations.

請求項2に記載の発明によれば、石油系液体燃料である重油や軽油を、安定した前記燃焼装置の燃料油とすることができる。  According to the invention described in claim 2, heavy oil or light oil, which is a petroleum-based liquid fuel, can be used as a stable fuel oil for the combustion apparatus.

請求項3に記載の発明によれば、酵素を混入することによって、燃料効率の高い前記燃焼装置の燃料油を製造できる。  According to invention of Claim 3, the fuel oil of the said combustion apparatus with high fuel efficiency can be manufactured by mixing an enzyme.

請求項4に記載の発明では、請求項1乃至3の何れか1項に記載の加水燃料油の製造方法により生成してあり、加水燃料油の原料油の量を65〜75%の割合にしてなるので、加水燃料油は、完全燃焼するから、燃料効率を高めることができる。  In invention of Claim 4, it produces | generates by the manufacturing method of the hydrofuel oil of any one of Claims 1 thru | or 3, and makes the quantity of the feedstock of hydro fuel oil into the ratio of 65 to 75%. Therefore, since the hydrolyzed fuel oil is completely burned, the fuel efficiency can be improved.

この発明の加水燃料の生成装置の概要を示すブロック図。The block diagram which shows the outline | summary of the production | generation apparatus of the water fuel of this invention. この発明の加水燃料の製造方法を示す工程図。The process drawing which shows the manufacturing method of the water fuel of this invention.

以下、この発明における加水燃料油の製造方法および加水燃料油の実施の形態について説明する。この発明の実施の形態は、発明の最も好ましい形態を示すものであり、この発明はこれに限定されない。  Hereinafter, the manufacturing method of the hydrofuel oil and embodiment of the hydrofuel oil in this invention are demonstrated. The embodiment of the present invention shows the most preferable mode of the present invention, and the present invention is not limited to this.

この発明における実施の形態を、図1および図2に基づいて説明する。図1は加水燃料油の生成装置の概要を示すブロック図であり、符号1は水道水、井戸水などの原水を収容する水タンク1で、この水タンク1内には、酸化還元装置8が設置され、前記原水が前記酸化還元装置8により電気分解され還元水になる。なお、符号9は前記酸化還元装置8の制御部で、電気分解の電圧を調整する。  An embodiment of the present invention will be described with reference to FIGS. FIG. 1 is a block diagram showing an outline of an apparatus for producing hydrofuel oil. Reference numeral 1 denotes a water tank 1 for storing raw water such as tap water and well water, and an oxidation-reduction device 8 is installed in the water tank 1. Then, the raw water is electrolyzed by the redox device 8 to be reduced water. Reference numeral 9 denotes a control unit of the oxidation-reduction apparatus 8 that adjusts the voltage of electrolysis.

前記水タンク1には、高圧ポンプ6にラインミキサー7が接続された第1循環路12が構成され、この第1循環路12には、前記水タンク1の流出側に位置する第1開閉バルブ15と、前記水タンク1の流入側に位置する第2開閉バルブ16が介在される。  The water tank 1 includes a first circulation path 12 in which a line mixer 7 is connected to a high-pressure pump 6. The first circulation path 12 includes a first opening / closing valve located on the outflow side of the water tank 1. 15 and a second on-off valve 16 located on the inflow side of the water tank 1 is interposed.

符号4は混合油タンクで、この混合油タンク4に原油料タンク2より、灯油、A重油、軽油などの石油系液体燃料よりなる原料油が供給されるとともに、添加剤タンク3より精製鉱物油および界面活性剤、溶剤などの混合物などの添加剤が供給される。  Reference numeral 4 denotes a mixed oil tank. The mixed oil tank 4 is supplied with raw material oil such as kerosene, heavy fuel oil A, and light oil from the crude oil tank 2 and refined mineral oil from the additive tank 3. And additives such as mixtures of surfactants, solvents and the like.

前記混合油タンク4には、前記高圧ポンプ6と前記ラインミキサー7が接続された第2循環路13が構成され、この第2循環路13には、前記混合油タンク4の流入側に位置する第3開閉バルブ17と、前記混合油タンク4の流出側に位置する第4開閉バルブ18が介在される。  The mixed oil tank 4 includes a second circulation path 13 to which the high-pressure pump 6 and the line mixer 7 are connected. The second circulation path 13 is located on the inflow side of the mixed oil tank 4. A third on-off valve 17 and a fourth on-off valve 18 located on the outflow side of the mixed oil tank 4 are interposed.

符号5は油水静置タンクで、この油水静置タンク5の流入側に位置する第5開閉バルブ19を介して前記第2循環路13に接続されるとともに、前記油水静置タンク5の流出側はバーナー、ボイラーなどの燃焼装置Fに接続される。  Reference numeral 5 denotes an oil / water stationary tank, which is connected to the second circulation path 13 via a fifth open / close valve 19 located on the inflow side of the oil / water stationary tank 5 and is also connected to the outflow side of the oil / water stationary tank 5. Is connected to a combustion device F such as a burner or boiler.

前記高圧ポンプ6の吐出側には調整バルブ20を介在し、前記高圧ポンプ6の吐出圧を調整し、圧力計21により前記高圧ポンプ6の吐出圧が表示させる。
なお、前記第1開閉バルブ15から前記第5開閉バルブ19および前記調整バルブ20は手動または電磁バルブのいずれでもよい。
An adjustment valve 20 is interposed on the discharge side of the high-pressure pump 6 to adjust the discharge pressure of the high-pressure pump 6 and the pressure gauge 21 displays the discharge pressure of the high-pressure pump 6.
The first on-off valve 15 to the fifth on-off valve 19 and the adjustment valve 20 may be either manual or electromagnetic valves.

前記混合油タンク4には電動モータ10が設置され、この電動モータ10に連結した回転翼11により前記混合油タンク4内の混合油または混合油水を攪半できるようにしたが、通常は、前記高圧ポンプ6より前記ラインミキサー7を通過する際の流通圧により前記混合油タンク4内が撹拌される。なお、符号14は前記混合油タンク4に設けたレベルセンサーで、前記混合油タンク4内の前記混合油水の上限を検出する。  An electric motor 10 is installed in the mixed oil tank 4, and the mixed oil or the mixed oil water in the mixed oil tank 4 can be stirred by the rotary blades 11 connected to the electric motor 10. The inside of the mixed oil tank 4 is agitated by the flow pressure when passing through the line mixer 7 from the high-pressure pump 6. Reference numeral 14 denotes a level sensor provided in the mixed oil tank 4 to detect the upper limit of the mixed oil water in the mixed oil tank 4.

この実施の態様において、第1工程では、まず、前記第3開閉バルブ17と前記第4開閉バルブ18および前記第5開閉バルブ19を閉じ、前記第1開閉バルブ15及び前記第2開閉バルブ16を開いて、前記水タンク1内で、前記酸化還元装置8により酸化還元した前記還元水を、前記水タンク1に前記高圧ポンプ6と前記ラインミキサー7とが接続される前記第1循環路12で所要時間循環させる。  In this embodiment, in the first step, first, the third on-off valve 17, the fourth on-off valve 18, and the fifth on-off valve 19 are closed, and the first on-off valve 15 and the second on-off valve 16 are closed. The reduced water that has been opened and oxidized / reduced by the oxidation / reduction device 8 in the water tank 1 is passed through the first circulation path 12 where the high-pressure pump 6 and the line mixer 7 are connected to the water tank 1. Circulate the required time.

前記第1循環路12を循環する前記還元水が前記高圧ポンプ6を通過する際、前記還元水に圧力と温度がかかるとともに、前記ラインミキサー7により微粒化されて前記水タンク1内に噴出し、前記水タンク1内で攪半される前記還元水をイオン化融合に近い状態にする。  When the reduced water circulating through the first circulation path 12 passes through the high-pressure pump 6, pressure and temperature are applied to the reduced water, and are atomized by the line mixer 7 and ejected into the water tank 1. The reduced water stirred in the water tank 1 is brought into a state close to ionization fusion.

次に、第2工程では、まず、前記第2開閉バルブ16を閉じ、前記第3開閉バルブ17を開くと、前記水タンク1の前記還元水が前記高圧ポンプ6より前記ラインミキサー7を通過して前記混合油タンク4に噴出し、前記混合油タンク4内を攪半しながら前記還元水が前記原料油と前記添加剤とに混合される。その後、前記第1開閉バルブ15を閉じ、前記第4開閉バルブ18を開くと、前記混合油タンク4内の前記混合油水が前記混合油タンク4に前記高圧ポンプ6と前記ラインミキサー7とが接続された第2循環路13を所要時間循環することにより、前記混合油タンク4内でエマルジョン化した加水燃料油が生成される。  Next, in the second step, first, when the second on-off valve 16 is closed and the third on-off valve 17 is opened, the reduced water in the water tank 1 passes through the line mixer 7 from the high-pressure pump 6. Then, the reduced water is mixed into the raw material oil and the additive while spraying into the mixed oil tank 4 and stirring the mixed oil tank 4. Thereafter, when the first opening / closing valve 15 is closed and the fourth opening / closing valve 18 is opened, the mixed oil in the mixed oil tank 4 is connected to the mixed oil tank 4 between the high pressure pump 6 and the line mixer 7. By circulating the second circulation path 13 for a required time, the hydrolyzed fuel oil emulsified in the mixed oil tank 4 is generated.

さらに、第3工程では、前記第5開閉バルブ19を開き、前記混合油タンクのエマルジョン化した前記加水燃料油を前記油水静置タンク5内に供給し、所要時間静置させて前記加水燃料油を前記燃焼装置Fの燃料油として送り出す。なお、前記油水静置タンク5内で前記加水燃料油を所要時間静置させることによって、前記油水静置タンク5内で上側の透明層部と下側に沈降した油分を含む乳白層部とに分離され、その透明層部を前記燃焼装置Fの前記燃料油として取り出し、前記バーナー、ボイラーなどの前記燃焼装置Fに供給して燃焼の安定性を維持する。  Further, in the third step, the fifth open / close valve 19 is opened, and the hydrolyzed fuel oil emulsified in the mixed oil tank is supplied into the oil / water static tank 5 and allowed to stand for a required time to allow the hydrolyzed fuel oil to remain. Is sent out as fuel oil of the combustion device F. In addition, by allowing the hydrolyzed fuel oil to stand in the oil / water static tank 5 for a required time, an upper transparent layer portion and a milky white layer portion containing oil that has settled downward in the oil / water static tank 5 are obtained. The separated transparent layer portion is taken out as the fuel oil of the combustion device F and supplied to the combustion device F such as a burner or a boiler to maintain combustion stability.

なお、この実施の態様では、前記混合油タンク4に前記原料油と前記添加剤よりなる前記混合油を供給しているが、前記混合油タンク4に前記酵素タンク22を接続し、前記混合油に酵素をさらに混入してもよい。  In this embodiment, the mixed oil composed of the raw material oil and the additive is supplied to the mixed oil tank 4, but the enzyme tank 22 is connected to the mixed oil tank 4, and the mixed oil An enzyme may be further mixed in.

以上のように、この発明においては、前記高圧ポンプ6および前記ラインミキサー7を前記第1工程の前記第1循環路12と前記第2工程の第2循環路13とに併用でき、しかも前記高圧ポンプ6は第3工程の前記油水静置タンク5に送り出すことに使われ、部品数を削減でき構造が簡素化され、設備が小型化できる。  As described above, in the present invention, the high pressure pump 6 and the line mixer 7 can be used in combination with the first circuit 12 in the first step and the second circuit 13 in the second step, and the high pressure The pump 6 is used for sending out to the oil / water stationary tank 5 in the third step, so that the number of parts can be reduced, the structure is simplified, and the equipment can be downsized.

また、前記酸化還元装置8により還元した還元水を前記高圧ポンプ6と前記ラインミキサー7を有する第1循環路12で所要時間循環されることにより微粒化するとともに、前記混合油水も前記高圧ポンプ6と前記ラインミキサー7を有する前記第2循環路13で所要時間循環されることにより微粒化し、イオン化融合に近い状態になるので、前記加水燃料油は分離し難く、前記原料油が減少しても燃焼安定性は低下することがなく、原料油のコスト削減をすることができる。  Further, the reduced water reduced by the oxidation-reduction device 8 is pulverized by circulating through the first circulation path 12 having the high-pressure pump 6 and the line mixer 7 for a required time, and the mixed oil water is also converted into the high-pressure pump 6. And the second circulation path 13 having the line mixer 7 is pulverized for a required time to be atomized and close to ionization fusion, so that the hydrofuel oil is difficult to separate and even if the feedstock oil is reduced Combustion stability does not decrease, and the cost of the feedstock can be reduced.

この発明の加水燃料油の製造方法および加水燃料油は、完全燃焼するから、燃料効率を高めることができ、バーナーあるいはボイラーなどの燃焼装置に適用できる。  Since the method for producing water and fuel oil according to the present invention completely burns, the fuel efficiency can be improved, and it can be applied to a combustion apparatus such as a burner or a boiler.

1 水タンク
2 原料油タンク
3 添加剤タンク
4 混合油タンク
5 油水静置タンク
6 高圧ポンプ
7 ラインミキサー
8 酸化還元装置
9 制御部
10 電動モータ
11 撹拌翼
12 第1循環路
13 第2循環路
14 レベルセンサー
15 第1開閉バルブ
16 第2開閉バルブ
17 第3開閉バルブ
18 第4開閉バルブ
19 第5開閉バルブ
20 調整バルブ
21 圧力計
22 酵素タンク
F 燃焼装置
DESCRIPTION OF SYMBOLS 1 Water tank 2 Raw material oil tank 3 Additive tank 4 Mixed oil tank 5 Oil-water stationary tank 6 High pressure pump 7 Line mixer 8 Oxidation reduction device 9 Control part 10 Electric motor 11 Stirring blade 12 1st circulation path 13 2nd circulation path 14 Level sensor 15 First on-off valve 16 Second on-off valve 17 Third on-off valve 18 Fourth on-off valve 19 Fifth on-off valve 20 Adjustment valve 21 Pressure gauge 22 Enzyme tank F Combustion device

Claims (4)

原水を酸化還元装置により還元した後、この還元水を、水タンクに高圧ポンプとラインミキサーとが接続される第1循環路にて所要時間循環させる第1工程と、原料油と添加剤との混合油を、混合油タンクに前記高圧ポンプと前記ラインミキサーとが接続される第2循環路にて所要時間循環させた後、前記第1工程にて循環させた前記還元水と、前記第2循環路で循環させた前記混合油との混合油水を前記第2循環路にてさらに所要時間循環させる第2工程と、前記混合油タンク内にてエマルジョン化した加水燃料油を油水静置タンク内で所要時間静置させ、燃焼装置の燃料油として送り出す第3工程とを含むことを特徴とする加水燃料油の製造方法。  After the raw water is reduced by the oxidation-reduction device, the reduced water is circulated for a required time in a first circulation path in which a high-pressure pump and a line mixer are connected to the water tank, and the raw oil and the additive The mixed oil is circulated for a required time in a second circulation path where the high pressure pump and the line mixer are connected to a mixed oil tank, and then the reduced water circulated in the first step, and the second A second step of circulating the mixed oil water with the mixed oil circulated in the circulation path for a further required time in the second circulation path; and the hydrolyzed fuel oil emulsified in the mixed oil tank in the oil-water stationary tank And a third step of leaving the fuel for a required time and sending it out as fuel oil for the combustion apparatus. 上記請求項1に記載の加水燃料油の製造方法において、原料油は、石油系液体燃料からなることを特徴とする加水燃料油の製造方法。  2. The method for producing a hydrolyzed fuel oil according to claim 1, wherein the raw material oil is composed of petroleum liquid fuel. 上記請求項1または2の何れか1項に記載の加水燃料油の製造方法において、混合油には酵素を混入することを特徴とする。  3. The method for producing a hydrofuel oil according to claim 1, wherein an enzyme is mixed in the mixed oil. 請求項1乃至3の何れか1項に記載の加水燃料油の製造方法により生成してあり、加水燃料油内の前記原料油の容量を65〜75%の割合にしてなることを特徴とする加水燃料油。  It is produced | generated by the manufacturing method of the hydrolyzed fuel oil of any one of Claim 1 thru | or 3, The capacity | capacitance of the said raw material oil in hydrous fuel oil is made into the ratio of 65 to 75%, It is characterized by the above-mentioned. Hydrous fuel oil.
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JP2008150421A (en) * 2006-12-14 2008-07-03 Kenji Suzuki Emulsion fuel, and manufacturing method and manufacturing apparatus thereof
JP2009191261A (en) * 2008-01-15 2009-08-27 Yoshisuke Nagao Method for producing emulsion fuel
JP2013119621A (en) * 2011-12-09 2013-06-17 Biotope:Kk Method for manufacturing fuel oil
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001348581A (en) * 2000-06-08 2001-12-18 Shigemi Sawada Apparatus and method for micronizing liquid molecular cluster
JP2008081740A (en) * 2006-09-01 2008-04-10 Sg Engineering Kk Method for producing emulsion fuel by mixing water and combustible oil in fine particle state, device for producing emulsion fuel and emulsion fuel
JP2008150421A (en) * 2006-12-14 2008-07-03 Kenji Suzuki Emulsion fuel, and manufacturing method and manufacturing apparatus thereof
JP2009191261A (en) * 2008-01-15 2009-08-27 Yoshisuke Nagao Method for producing emulsion fuel
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